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The Gibbs Phase Rule and its Application, Lecture notes of Chemistry

Binary solid-liquid Equilibrium, Melting Point Variation with Composition

Typology: Lecture notes

2020/2021

Uploaded on 05/24/2021

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Colby College
Gibbs Phase Rule: f = c – p + 2
f = Intensive Degrees of freedom = variance
Number of intensive variables that can be changed independently without
disturbing the number of phases in equilibrium
p = number of phases
gas, homogeneous liquid phases, homogeneous solid phases
c = components
Minimum number of independent constituents
Case I. No chemical reactions: c = constituents
Example 1: start with methanol and water – 2 components
Case II With chemical reactions:
Example 2: start with NaH
2
PO
4
in water --
K
a2
K
a3
H
2
PO
4-
HPO
42-
+ H
+
PO
43-
+ H
+
Constituents: Na
+
, H
+
, H
2
PO
4-
, HPO
42-
, PO
43-
, H
2
O
but only 2 components -- NaH
2
PO
4
and H
2
O.
Example 3: start with NaH
2
PO
4
and Na
2
HPO
4
in water --
Same constituents: Na
+
, H
+
, H
2
PO
4-
, HPO
42-
, PO
43-
, H
2
O
but now 3 components -- NaH
2
PO
4
, Na
2
HPO
4
, and H
2
O.
Need to know: T, P, y
A
, y
B
, x
A
, x
B
total intensive variables = c p + 2
But y
A
+ y
B
= 1
x
A
+ x
B
= 1
Get p such equations, one for each phase:
Independent variables = c p + 2 – p
But, chemical potential is everywhere equal:
µ
A
(x
A
) = µ
A
(g)
µ
B
(x
B
) = µ
B
(g)
Get p–1 for each component
Get c( p–1) such equations:
Independent variables = c p + 2 – p – c( p–1)
f = c – p + 2
A & B
liquid
µ
A
(g)
µ
A
(x
A
)
=
µ
B
(x
B
)
=
µ
B
(g)
x
A
+ x
B
=1
A & B
vapor
y
A
+ y
B
=1
f ' = c – p + 1
P = cst
0 1
x
A
,
y
A
liquid A & B
f ' = 2
vapor A & B
T f ' = 1
f ' = 2
T
*
bA
T
*
bB
pf2

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Colby College

Gibbs Phase Rule: f = c – p + 2

f = Intensive Degrees of freedom = variance Number of intensive variables that can be changed independently without disturbing the number of phases in equilibrium

p = number of phases gas, homogeneous liquid phases, homogeneous solid phases

c = components Minimum number of independent constituents Case I. No chemical reactions: c = constituents Example 1 : start with methanol and water – 2 components Case II With chemical reactions: Example 2 : start with NaH 2 PO 4 in water -- Ka2 Ka H 2 PO 4 -^ →← HPO 4 2-^ + H+^ →← PO 4 3-^ + H+ Constituents: Na+, H+, H 2 PO 4 - , HPO 4 2-, PO 4 3-, H 2 O but only 2 components -- NaH 2 PO 4 and H 2 O. Example 3 : start with NaH 2 PO 4 and Na 2 HPO 4 in water -- Same constituents: Na+, H+, H 2 PO 4 - , HPO 4 2-, PO 4 3-, H 2 O but now 3 components -- NaH 2 PO 4 , Na 2 HPO 4 , and H 2 O.

Need to know: T, P, y A, y B, x A, x B

total intensive variables = c p + 2

But y A + y B = 1

x A + x B = 1 Get p such equations, one for each phase:

Independent variables = c p + 2 – p

But, chemical potential is everywhere equal: μA( x A) = μA(g) μB( x B) = μB(g) Get p–1 for each component Get c( p–1) such equations: Independent variables = c p + 2 – p – c( p–1)

f = c – p + 2

A & B liquid

μA(g) μA( x A)

μB( x B)

μB(g)

x A + x B =

A & B vapor

y A + y B =

f ' = c – p + 1 P = cst

(^0) x A, y A →^1

liquid A & B f ' = 2

vapor A & B

T (^) f ' = 1

f ' = 2

T (^) bA*

T (^) bB*

Colby College

f ' = c – p + 1 cst. P f "= c – p cst. T&P

Binary solid-liquid Equilibrium Melting Point Variation with Composition c = 2 p = 3

liquid, pure solid A, pure solid B

Solid-liquid 2-phase region: f ' = 2 – 2 + 1 = 1

Eutectic: f ' = 2 – 3 + 1 = 0 invariant at cst P

For NaCl in water: Eutectic -21.1 oC at 23% wt/wt giving NaCl·2H 2 O

Add One Extensive Independent Variable for Each Phase: Gibbs energy is extensive: Degrees of freedom:

D = f + p

Binary Solid-Liquid at constant T & P:

Solid-liquid 2-phase region: f " = 2 – 2 = 0 D " = f " + p = 0 + 2 = 2

dG = μA dnA + μB dnB dnA and dnB: totals for both phases

since: μA(s) = μA(l), and μB(s) = μB(l) (doesn’t matter which phase)

A & B liquid

Solid A & Solid B

P = cst

(^0) x A → 1

solid A & solid B

liquid A & B T f ' = liq. & solid B

f ' = liq. & solid A f ' =

f ' =

f ' = c – p + 1